CN104973707A - Seasonal high turbidity raw water processing technology - Google Patents
Seasonal high turbidity raw water processing technology Download PDFInfo
- Publication number
- CN104973707A CN104973707A CN201510370648.2A CN201510370648A CN104973707A CN 104973707 A CN104973707 A CN 104973707A CN 201510370648 A CN201510370648 A CN 201510370648A CN 104973707 A CN104973707 A CN 104973707A
- Authority
- CN
- China
- Prior art keywords
- water
- tank
- preliminary sedimentation
- concentration
- mud
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Treatment Of Sludge (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a seasonal high turbidity raw water processing technology. The technology comprises the following steps: introducing raw water into a pre-setting, condensing, and reusing tank to carry out pre-setting, then introducing the effluent into a settling tank to carry out settling, introducing the effluent into a filtration tank to filter the water, storing the effluent in a clear water tank, pressurizing the clear water by a secondary pump house to pump the clear water into municipal pipe network; storing the sludge discharged from the pre-setting, condensing, and reusing tank in a balance tank, dehydrating the sludge in a dehydration chamber, transporting the dehydrated sludge out of the system, and introducing the filtrate to a condensation mass-energy conversion tank. The provided technology can adapt to different raw water and meet different operation requirements; the sludge water processing technology and water purification technology are combined together; the technology can be operated under the work situations of seasonal high turbidity and usual low turbidity; the supernate in the concentration tank and dehydration filtrate, which usually exceed the standards in the waste water concentration and dehydration technology, are subjected to a secondary treatment in the concentration mass-energy conversion tank, the structure foundation processing ability is utilized efficiently so as to reduce the floor surface, the discharged water can meet the discharge standards, and the organic substances in waste water are converted into biological energy, which can be further utilized.
Description
The present invention is the applying date is on July 30th, 2014, and application number is the divisional application of the patent application " seasonal high turbid original sub-block technique " of 201410368768.4.
Technical field
The present invention is that the one related in water supply and sewage work tackles seasonal high turbidity raw sewage treatment process, is specifically a kind ofly applied to the combined treatment process of taking seasonal high turbidity raw sewage waterworks.For the high turbidity raw sewage that seasonality occurs, former water preliminary sedimentation and sludge condensation process are combined, realize water factory's effluent quality under the different operating mode of former water height low turbidity up to standard, and realize producing concentrated, the dehydration of mud and the optimum combination treatment process of characteristic energy changes simultaneously.
Background technology
Containing gas chromatography and inorganics in the water inlet of city tap-water factory, earth surface water source is subject to the factors vary such as flow and water temperature at the change of season, occur that turbidity significantly raises in short-term, water factory's treatment scheme cannot be tackled, produce a large amount of factory effluent simultaneously and discharge technical process as production by product, larger pressure is produced to surrounding enviroment, becomes environment and social concern that city tap-water factory must solve.
At present, before conventional sedimentation and filtration process, generally adopt simple preliminary sedimentation procedure to deal with the seasonal high turbidity water quality occurred in the waterworks of taking high turbidity raw sewage, and contained mud impurity is often treated as source of pollution in factory effluent, by concentrated, natural mummification or mechanical dehydration, contained production mud in factory effluent is transported outward with the form of solid body, to reduce the impact on environment.The main drawback of above-mentioned technology is after ultra, raw water of waterworks present continue comparatively low turbidity time, preliminary sedimentation procedure cannot play a role in treatment process, and factory effluent drain time is generally comparatively concentrated, process structures floor space is comparatively large, and running cost is higher, and concentrated supernatant and dehydration filtrate are often more difficult reaches emission standard, wherein large amount of organic becomes environmental pressure again as pollutent, has become the technical barrier of seasonal high turbidity raw sewage process.
Summary of the invention
The object of this invention is to provide a kind of seasonal high turbid original sub-block technique, be suitable for the combined treatment process under seasonal high turbidity raw sewage condition, overcome the conventional art prejudice that water and mud process respectively, preliminary sedimentation process, sedimentation and filtration, sludge concentration and dewatering and waste water reclamation and characteristic energy changes function are combined, while guaranteeing that treatment process effluent quality is up to standard, the thickening of realization production spoil disposal water, sludge treatment tail water qualified discharge and Organic substance in water are converted into the function that bioenergy reclaims further.
To achieve these goals, technical scheme of the present invention is: a kind of seasonal high turbid original sub-block technique, it is characterized in that former water is introduced into after preliminary sedimentation concentrates reuse tank preliminary sedimentation, water outlet enters settling tank precipitation, after precipitation water outlet enters filter, water outlet enters after clean water basin regulate and store, pressurizeed by repumping house and send into city planting ductwork, the spoil disposal access counterbalance cell that preliminary sedimentation concentrates reuse tank stores, mud extraction enters dehydration machine room and carries out processed, deviate from the outward transport of dry mud to dispose, filtrate enters concentration mass energy conversion pool.
According to embodiments of the invention, when water factory's land used is well-to-do and construction fund is more nervous, depositing technology can consider the horizontal sedimentation tank that employing floor space is larger or tube settler, horizontal sedimentation tank or tube settler spoil disposal access spoil disposal pond after promote enter concentration basin concentrate, concentration basin supernatant liquor enters concentration mass energy conversion pool, and concentration basin spoil disposal and preliminary sedimentation concentrate reuse tank spoil disposal and after counterbalance cell is regulated and stored, enter dehydration machine room in the lump carry out processed.
After filter cell rinse waste water enters blowoff basin, with former water mixing reuse after general lifting, under emergency condition, enter concentration mass energy conversion pool.Concentration mass energy conversion pool accepts dehydration machine room filtrate and blowoff basin and meets an urgent need after draining and carry out in-depth process, and partial organic substances is converted into bioenergy and reclaims, and all the other mud carry out sludge drying process; Concentration mass energy conversion pool filtrate can enter blowoff basin promote after as former water conservancy use, or up to standardly enter river water body.At ordinary times during low turbidity operating mode raw water turbidity lower than 200NTU or sediment concentration lower than 0.20 kg/m
3, former water can surmount preliminary sedimentation and concentrate reuse tank and directly enter settling tank process; When raw water turbidity more than 200NTU or sediment concentration at 0.20 ~ 3.5kg/m
3time, former water first should concentrate after reuse tank preliminary sedimentation through preliminary sedimentation and enter settling tank process again; When former water sediment concentration is more than 3.5kg/m
3time, former water first should be introduced into settling pit sand setting at dry point place, and water outlet concentrates reuse tank through preliminary sedimentation again and enters settling tank process.Before sediment outflow pond and preliminary sedimentation concentrate reuse tank, add potassium permanganate, add PAM, before efficient sedimentation tank, add alum before sediment outflow pond and preliminary sedimentation concentrate reuse tank He in efficient sedimentation tank, chlorination before and after clean water basin, adds burgy after settling pit.
Sand setting process, sedimentation and filtration, sludge concentration and dewatering and waste water reclamation and characteristic energy changes function combine by the present invention, first the Treatment for Reuse of factory effluent and preliminary sedimentation are combined, be arranged on settling tank in the past as a part for water-purifying process, and the supernatant liquor produced in wastewater treatment and dehydration filtrate are carried out characteristic energy changes, the organism of part is converted into bioenergy.The different coprecipitation modes that the present invention adopts according to treatment process, classify treatment process, then according to different operational conditionss and requirement, form the complete process system of two cover treatment process compositions.The advantage of this technique is to adapt to different former regimen condition and operating requirement, water for drainage slurry technique and water-purifying process are combined, the seasonal high concentrtion of simultaneous adaptation and at ordinary times low turbidity operating mode, factory effluent is concentrated with dewatering process in be easy to the concentration basin supernatant liquor of discharge beyond standards and dehydration filtrate concentration mass energy conversion pool carries out secondary treatment, efficiency utilization structures processing power, to save floor occupying area, realizes organism in the discharge of water-purifying process standard water discharge and factory effluent and is converted into the effect that bioenergy reclaims further.
Accompanying drawing explanation
Fig. 1 is for efficient sedimentation tank process seasonal ultra's treatment process schematic diagram.
Fig. 2 is for employing horizontal sedimentation tank or tube settler process seasonal ultra's treatment process schematic diagram.
Fig. 3 is the structural representation that preliminary sedimentation concentrates reuse tank.
Fig. 4 is the A-A sectional view of Fig. 3.
Fig. 5 is the B-B sectional view of Fig. 3.
Fig. 6 is adjustable perforation effluent trough floor plan schematic diagram.
Fig. 7 is adjustable perforation effluent trough side arrangement schematic diagram.
Fig. 8 is the sectional view of adjustable perforation effluent trough along C-C line in Fig. 7.
Fig. 9 is the sectional view of adjustable perforation effluent trough along D-D line in Fig. 7.
Figure 10 is that adjustable profile of tooth weir plate effluent trough arranges schematic diagram.
Figure 11 is the profile of tooth weir plate detail drawing of adjustable profile of tooth weir plate effluent trough.
Figure 12 is the weir plate pad detail drawing of adjustable profile of tooth weir plate effluent trough.
Embodiment
Below in conjunction with accompanying drawing, the invention will be further described.
The present invention is a kind of seasonal ultra's treatment process, first according to situations such as water factory's land used and funds, treatment process is divided into the seasonal ultra's treatment process of efficient sedimentation tank process and horizontal sedimentation tank or tube settler process seasonal ultra's treatment process two class.When water factory place is nervous and construction fund is well-to-do, depositing technology can be considered to adopt occupation of land face little and the efficient sedimentation tank of band sludge reflux and concentrating function; When water factory's land used is well-to-do and construction fund is more nervous, depositing technology can consider the horizontal sedimentation tank that employing occupation of land face is larger or tube settler.At ordinary times during low turbidity operating mode raw water turbidity lower than 200NTU or sediment concentration lower than 0.20 kg/m
3, former water can surmount preliminary sedimentation and concentrate reuse tank and directly enter settling tank process; When raw water turbidity more than 200NTU or sediment concentration at 0.20 ~ 3.5kg/m
3time, former water first should concentrate after reuse tank preliminary sedimentation through preliminary sedimentation and enter settling tank process again; When former water sediment concentration is more than 3.5kg/m
3time, former water first should be introduced into settling pit sand setting at dry point place, and water outlet concentrates reuse tank through preliminary sedimentation again and enters settling tank process.
Efficient sedimentation tank 2 processes in seasonal ultra's treatment process, former water 1 is introduced into after preliminary sedimentation concentrates reuse tank 2 preliminary sedimentation, and water outlet enters efficient sedimentation tank 3 and precipitates, and precipitation water outlet enters after filter tank 4 filters, water outlet enters after clean water basin 5 regulate and store, and is pressurizeed send into city planting ductwork 7 by repumping house 6.The spoil disposal access counterbalance cell 8 that preliminary sedimentation concentrates reuse tank 2 and efficient sedimentation tank 3 stores, and mud extraction enters dehydration machine room 9 and carries out processed, and deviate from the outward transport of dry mud and dispose, filtrate enters concentration mass energy conversion pool 10.After filter tank 4 flushing waste water enters blowoff basin 14, mix reuse with former water 1 after general lifting, under emergency condition, enter concentration mass energy conversion pool 10.Concentration mass energy conversion pool 10 accepts dehydration machine room 9 filtrate and blowoff basin 14 and meets an urgent need after draining and carry out in-depth process, and partial organic substances is converted into bioenergy and reclaims 11, and all the other mud carry out sludge drying and dispose 12; Concentration mass energy conversion pool 10 filtrate can enter blowoff basin 14 promote after as former water conservancy use, or up to standardly enter river water 13.When former water 1 sediment concentration is more than 3.5kg/m
3time, former water 1 is introduced into settling pit 15 sand setting at dry point place; When former water 1 turbidity lower than 200NTU or sediment concentration lower than 0.20 kg/m
3time, former water 1 can surmount preliminary sedimentation and concentrate reuse tank 2 and directly enter efficient sedimentation tank 3.Settling pit 15 and preliminary sedimentation concentrate reuse tank 2 regularly sediment outflow.Before settling pit 15 and preliminary sedimentation concentrate reuse tank 2, add potassium permanganate 16, before settling pit 15 and preliminary sedimentation concentrate reuse tank 2 He in efficient sedimentation tank 3, add PAM17, add alum 18 before efficient sedimentation tank 3, chlorination 19 before and after clean water basin 5, adds burgy 20 after settling pit 15.
Horizontal sedimentation tank 21 or tube settler 22 process in seasonal ultra's treatment process, former water 1 is introduced into after preliminary sedimentation concentrates reuse tank 2 preliminary sedimentation, water outlet enters horizontal sedimentation tank 21 or tube settler 22 precipitates, after precipitation water outlet enters filter tank 4 filtration, water outlet enters after clean water basin 5 regulate and store, and is pressurizeed send into city planting ductwork 7 by repumping house 6.The rear lifting of horizontal sedimentation tank 21 or tube settler 22 spoil disposal access spoil disposal pond 23 enters concentration basin 24 and concentrates, concentration basin 24 supernatant liquor enters concentration mass energy conversion pool 10, concentration basin 24 spoil disposal and preliminary sedimentation concentrate reuse tank 2 spoil disposal and after counterbalance cell 8 is regulated and stored, enter dehydration machine room 9 in the lump carry out processed, deviate from the outward transport of dry mud to dispose, filtrate enters concentration mass energy conversion pool 10.After filter tank 4 flushing waste water enters blowoff basin 14, mix reuse with former water 1 after general lifting, under emergency condition, enter concentration mass energy conversion pool 10.Concentration mass energy conversion pool 10 accepts concentration basin 24 supernatant liquor, dehydration machine room 9 filtrate and blowoff basin 14 and meets an urgent need after draining and carry out in-depth process, and partial organic substances is converted into bioenergy and reclaims 11, and all the other mud carry out sludge drying process 12; Concentration mass energy conversion pool 10 filtrate can enter blowoff basin 14 promote after as former water conservancy use, or up to standardly enter river water 13.When former water 1 sediment concentration is more than 3.5kg/m
3time, former water 1 is introduced into settling pit 15 sand setting at dry point place; When former water 1 turbidity lower than 200NTU or sediment concentration lower than 0.20 kg/m
3time, former water 1 can surmount preliminary sedimentation and concentrate reuse tank 2 and directly enter horizontal sedimentation tank 21 or tube settler 22.Settling pit 15 and preliminary sedimentation concentrate reuse tank 2 regularly sediment outflow.Before sediment outflow pond 15 and preliminary sedimentation concentrate reuse tank 2, add potassium permanganate 16 and PAM17, before horizontal sedimentation tank 21 or tube settler 22, add alum 18, chlorination 19 before and after clean water basin 5, adds burgy 20 after settling pit 15.
Fig. 3 ~ Fig. 5 is the structural representation that a kind of preliminary sedimentation concentrates reuse tank, this preliminary sedimentation concentrates reuse tank and comprises pond body 30 and slush pump room 31, it is characterized in that the center water distribution bucket 32 that band distributing hole 57 is set in pond body 30 and the rectification bucket 53 be arranged on outside center water distribution bucket 32, described center water distribution bucket 32 is connected with the water inlet pipe 33 be arranged on bottom the body of pond, the weir plate 34 that the upper end-face edge of pond body 30 is provided with effluent trough and matches with effluent trough, effluent trough is connected with post precipitation pond by rising pipe 35, concentrated mud scraper 36 is set in pond body 30, mud-removing bucket 37 is set bottom the body of pond, set out sandpipe 38 bottom pond body 30 to be connected with mud-removing bucket 37, slush pump room 31 arranges water pump 42, unit fixed on water pump suction pipeline is installed manually-operated gate 39, exit of pump pipeline is installed vacuum breaker 40 and manually-operated gate 39, go out on sandpipe 38 and electrically operated valve 41 is also installed, the inlet pipeline of water pump 42 with go out sandpipe upstream and be connected by taking out sandpipe 43, the outlet conduit of water pump with go out sandpipe downstream and be connected by sediment outflow pipe 44, the inlet pipeline of water pump is connected with water inlet pipe by extraction mud pipe 45, the outlet conduit of water pump is also connected with shore pipe 46.Described effluent trough comprises the interior effluent trough 47 be arranged on inside the body of pond and the outer effluent trough 48 being arranged on external side, pond, and is communicated with the connective slot 49 of interior effluent trough 47 and outer effluent trough 48, and outer effluent trough 48 is connected with rising pipe 35.Pond body bottom sides is provided with evacuated tube 50.Water inlet pipe also arranges reuse water pipe 51 and is connected with plant area's blowoff basin 14 water side.Concentrate reclamation set upper and lower at preliminary sedimentation to arrange and rinse bolt 55, going out the washpipe 54 sandpipe arranging band vacuum breaker and manually-operated gate, as in pond and pipeline cleaning measure.PAM toss area 56 established by the water inlet pipe that preliminary sedimentation concentrates reclamation set.Water inlet pipe 33, go out on sandpipe 38 and blow-down pipe 50 to arrange valve well 52.
Wherein interior effluent trough and outer effluent trough use adjustable perforation effluent trough or adjustable profile of tooth weir plate effluent trough.
The structure of adjustable perforation effluent trough is as shown in Fig. 6 ~ 9, described adjustable effluent trough comprises perforation effluent trough 101, bottom perforation effluent trough 101, adjustable plate 104 is set, adjustable plate 104 is connected with screed 105 by adjusting bolt 106, screed 105 is fixed on and supports beam column or bracket 103 top, and perforation effluent trough 101 is also connected with support beam column or bracket 103 by fixing channel-section steel 102.Perforation effluent trough 101 is connected by joint bolt 109 with fixing channel-section steel 102, and fixing channel-section steel 102 is fixed on by standing bolt 108 and supports on beam column or bracket 103, and fixing channel-section steel 102 offers the strip adjustment hole 118 matched with standing bolt 108.Adjustable plate about 104 is respectively arranged with the regulating nut 107 matched with adjusting bolt 106.Establish communicating aperture 110 bottom perforation effluent trough 101, prosopyle 111 and water mark line 112 are established in side.When perforation effluent trough 101 regulates, first by regulating perforation effluent trough 101 both sides adjusting bolt 106 up-down adjustment nut 107 to make the water mark line 112 of effluent trough side overlap with pool inner water bit line, then tightening standing bolt 108, whole regulate process can be completed.
The structure of adjustable profile of tooth weir plate effluent trough is as shown in Figure 10 ~ 12, described adjustable profile of tooth weir plate effluent trough comprises Steel Concrete effluent trough 113, Steel Concrete effluent trough 113 is provided with profile of tooth weir plate 114, profile of tooth weir plate 114 is connected with Steel Concrete effluent trough 113 by weir plate pad 115, and profile of tooth weir plate 114 is also connected with Steel Concrete effluent trough 113 by back up pad 116.Profile of tooth weir plate 114 is connected with Steel Concrete effluent trough 113 with weir plate pad 115 by standing bolt 108; Back up pad 116 is connected with profile of tooth weir plate 114 by joint bolt 109, and profile of tooth weir plate 114 and weir plate pad 115 are provided with strip adjustment hole 118, and water mark line 112 is established in profile of tooth weir plate 114 side.When profile of tooth weir plate 114 regulates, first regulate back up pad 116 and profile of tooth weir plate 114 relative position that the water mark line 112 of profile of tooth weir plate 114 side is overlapped with pool inner water bit line by joint bolt 109, then tighten standing bolt 108, whole regulate process can be completed.
Former water concentrates the center water distribution bucket entering band distributing hole bottom the body of reuse tank pond from preliminary sedimentation by water inlet pipe, again by distributing hole and water distribution bucket water distribution, after preliminary sedimentation, water outlet enters interior effluent trough and outer effluent trough by weir plate, water outlet enters post precipitation pond by rising pipe after being pooled to outer effluent trough by connective slot connection, in water, mud is collected at mud-removing bucket after being concentrated by concentrated mud scraper, arranges outward by going out sandpipe.The water pump extracting mud is established in slush pump room, water inlet pipe and shake out blockage time, by extraction mud pipe with take out sandpipe and extract pipeline inner product mud and long-pending sand, drain into out sandpipe by sediment outflow pipe and to power on movable valve downstream, or enter plant area's sewage sludge storage system by shore pipe.
Described preliminary sedimentation concentrates reuse tank and the process of former water preliminary sedimentation and spoil disposal water concentration technique is combined, the seasonal high concentrtion of simultaneous adaptation and at ordinary times low turbidity operating mode, efficiency utilization structures processing power, to save floor occupying area, realizes the combination of water-purifying process and production wastewater treatment technique
Wherein settling pit, efficient sedimentation tank, horizontal sedimentation tank, tube settler, filter tank, clean water basin, repumping house, blowoff basin, spoil disposal pond, concentration basin, counterbalance cell, dehydration machine room and concentration mass energy conversion pool are prior art, no longer describe in detail.
Claims (7)
1. the high turbid original sub-block technique of seasonality, it is characterized in that former water is introduced into after preliminary sedimentation concentrates reuse tank preliminary sedimentation, water outlet enters settling tank precipitation, after precipitation water outlet enters filter, water outlet enters after clean water basin regulate and store, pressurizeed by repumping house and send into city planting ductwork, the spoil disposal access counterbalance cell that preliminary sedimentation concentrates reuse tank stores, mud extraction enters dehydration machine room and carries out processed, deviate from the outward transport of dry mud to dispose, filtrate enters concentration mass energy conversion pool, the horizontal sedimentation tank that settling tank adopts occupation of land face larger or tube settler, horizontal sedimentation tank or tube settler spoil disposal access spoil disposal pond after promote enter concentration basin concentrate, concentration basin supernatant liquor enters concentration mass energy conversion pool, concentration basin spoil disposal and preliminary sedimentation concentrate reuse tank spoil disposal and after counterbalance cell is regulated and stored, enter dehydration machine room in the lump carry out processed.
2. seasonal ultra's treatment process as claimed in claim 1, after it is characterized in that filter cell rinse waste water enters blowoff basin, with former water mixing reuse after general lifting, concentration mass energy conversion pool is entered under emergency condition, concentration mass energy conversion pool accepts dehydration machine room filtrate and blowoff basin and meets an urgent need after draining and carry out in-depth process, partial organic substances is converted into bioenergy and reclaims, and all the other mud carry out sludge drying disposal; Concentration mass energy conversion pool filtrate can enter blowoff basin promote after as former water conservancy use, or up to standardly enter river water.
3. as claim, the seasonal ultra's treatment process described in 1, it is characterized in that at ordinary times low turbidity operating mode time raw water turbidity lower than 200NTU or sediment concentration lower than 0.20 kg/m
3, former water surmounts preliminary sedimentation and concentrates reuse tank and directly enter settling tank process; When raw water turbidity more than 200NTU or sediment concentration at 0.20 ~ 3.5kg/m
3time, former water first concentrates after reuse tank preliminary sedimentation through preliminary sedimentation and enters settling tank process again; When former water sediment concentration is more than 3.5kg/m
3time, former water first should be introduced into settling pit sand setting at dry point place, and water outlet concentrates reuse tank through preliminary sedimentation again and enters settling tank process.
4. seasonal ultra's treatment process as claimed in claim 2, is characterized in that adding potassium permanganate before sediment outflow pond and preliminary sedimentation concentrate reuse tank, before sediment outflow pond and preliminary sedimentation concentrate reuse tank He in efficient sedimentation tank, adds PAM.
5. seasonal ultra's treatment process as claimed in claim 3, is characterized in that adding potassium permanganate and PAM before sediment outflow pond and preliminary sedimentation concentrate reuse tank.
6. seasonal ultra's treatment process as claimed in claim 1, it is characterized in that former water concentrates the center water distribution bucket entering band distributing hole bottom the body of reuse tank pond from preliminary sedimentation by water inlet pipe, again by distributing hole and water distribution bucket water distribution, after preliminary sedimentation, water outlet enters interior effluent trough and outer effluent trough by weir plate, water outlet enters post precipitation pond by rising pipe after being pooled to outer effluent trough by connective slot connection, in water, mud is collected at mud-removing bucket after being concentrated by concentrated mud scraper, arranges outward by going out sandpipe.
7. seasonal ultra's treatment process as claimed in claim 6, it is characterized in that in slush pump room, establishing the water pump extracting mud, water inlet pipe and shake out blockage time, by extraction mud pipe with take out sandpipe and extract pipeline inner product mud and long-pending sand, drain into out sandpipe by sediment outflow pipe to power on movable valve downstream, or enter plant area's sewage sludge storage system by shore pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510370648.2A CN104973707B (en) | 2014-07-30 | 2014-07-30 | A kind of seasonal high turbid original sub-block technique |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510370648.2A CN104973707B (en) | 2014-07-30 | 2014-07-30 | A kind of seasonal high turbid original sub-block technique |
| CN201410368768.4A CN104140166B (en) | 2014-07-30 | 2014-07-30 | Seasonal high turbid original sub-block technique |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410368768.4A Division CN104140166B (en) | 2014-07-30 | 2014-07-30 | Seasonal high turbid original sub-block technique |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104973707A true CN104973707A (en) | 2015-10-14 |
| CN104973707B CN104973707B (en) | 2018-04-20 |
Family
ID=51849521
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510370648.2A Active CN104973707B (en) | 2014-07-30 | 2014-07-30 | A kind of seasonal high turbid original sub-block technique |
| CN201410368768.4A Active CN104140166B (en) | 2014-07-30 | 2014-07-30 | Seasonal high turbid original sub-block technique |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410368768.4A Active CN104140166B (en) | 2014-07-30 | 2014-07-30 | Seasonal high turbid original sub-block technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (2) | CN104973707B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105396335A (en) * | 2015-12-18 | 2016-03-16 | 新昌中法供水有限公司 | Small and medium-sized water treatment plant sludge water treatment method |
| CN110448940A (en) * | 2018-05-07 | 2019-11-15 | 浙江联池水务设备股份有限公司 | A kind of water treatment plant's water for drainage slurry system and processing method |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115180700A (en) * | 2022-07-21 | 2022-10-14 | 安徽东至广信农化有限公司 | Tail water treatment process for water purification station |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202465420U (en) * | 2012-02-17 | 2012-10-03 | 上海市政工程设计研究总院（集团）有限公司 | Combined enhanced treatment device for seasonal metal-polluted raw water with low turbidity and high algae |
| JP5121983B1 (en) * | 2011-07-06 | 2013-01-16 | 磯村豊水機工株式会社 | Flocculant injection method and injection apparatus |
| CN103241856A (en) * | 2012-02-06 | 2013-08-14 | 上海市政工程设计研究总院（集团）有限公司 | Water treatment device for treating raw water with relatively large turbidity variation, and water treatment process thereof |
| CN203513453U (en) * | 2013-09-03 | 2014-04-02 | 上海市政工程设计研究总院（集团）有限公司 | Mass energy conversion treatment device for production waste water |
-
2014
- 2014-07-30 CN CN201510370648.2A patent/CN104973707B/en active Active
- 2014-07-30 CN CN201410368768.4A patent/CN104140166B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5121983B1 (en) * | 2011-07-06 | 2013-01-16 | 磯村豊水機工株式会社 | Flocculant injection method and injection apparatus |
| CN103241856A (en) * | 2012-02-06 | 2013-08-14 | 上海市政工程设计研究总院（集团）有限公司 | Water treatment device for treating raw water with relatively large turbidity variation, and water treatment process thereof |
| CN202465420U (en) * | 2012-02-17 | 2012-10-03 | 上海市政工程设计研究总院（集团）有限公司 | Combined enhanced treatment device for seasonal metal-polluted raw water with low turbidity and high algae |
| CN203513453U (en) * | 2013-09-03 | 2014-04-02 | 上海市政工程设计研究总院（集团）有限公司 | Mass energy conversion treatment device for production waste water |
Non-Patent Citations (1)
| Title |
|---|
| 许嘉炯等: "新型中置式高密度沉淀池的开发与应用", 《给水排水》 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105396335A (en) * | 2015-12-18 | 2016-03-16 | 新昌中法供水有限公司 | Small and medium-sized water treatment plant sludge water treatment method |
| CN105396335B (en) * | 2015-12-18 | 2018-04-03 | 新昌中法供水有限公司 | A kind of middle-size and small-size water treatment plant's water for drainage slurry technique |
| CN110448940A (en) * | 2018-05-07 | 2019-11-15 | 浙江联池水务设备股份有限公司 | A kind of water treatment plant's water for drainage slurry system and processing method |
| CN110448940B (en) * | 2018-05-07 | 2024-01-23 | 浙江联池水务设备股份有限公司 | Mud water treatment system and mud water treatment method for water purification plant |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104140166A (en) | 2014-11-12 |
| CN104973707B (en) | 2018-04-20 |
| CN104140166B (en) | 2016-02-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103408194B (en) | Small sewage treatment hydrolysis and gas-stripping and precipitation technique method | |
| CN101318735B (en) | Sewage water denitrification processing method of artificial rapid infiltration system and application thereof | |
| CN104140166B (en) | Seasonal high turbid original sub-block technique | |
| CN103288243A (en) | A system and a method for recycling coal mine drainage and power plant waste water with zero discharge | |
| CN102295387B (en) | Device and method for processing high-density landfill leachate | |
| CN202246296U (en) | Device for deeply purifying and treating high eutrophic water | |
| CN102329021B (en) | High-eutrophication water advanced purification treatment method and device | |
| CN203154885U (en) | V-shaped sedimentation tank | |
| CN207608952U (en) | Rainwater-collecting and processing unit | |
| CN101209885A (en) | Wastewater treatment method of garbage leachate | |
| CN104418481A (en) | Mass-energy transformation treatment process for production wastewater | |
| CN106698848A (en) | Miniaturized sewage treatment system | |
| CN204058089U (en) | Seasonal high turbid original sub-block device | |
| CN205170624U (en) | Environmental protection sewage treatment system | |
| CN102535624B (en) | Sewage concentration drainage device | |
| CN205387512U (en) | Wastewater treatment device | |
| CN206051798U (en) | Sewage pre-treatment integrated apparatus | |
| CN108557966A (en) | The processing method of coal yard coal-contained wastewater | |
| CN203701248U (en) | Comprehensive recycling device for waste water resource of thermal power plant | |
| CN203451279U (en) | Activated sludge sewage treatment device | |
| CN202822884U (en) | Inclined tube or inclined plate sedimentation tank with sludge concentration function | |
| CN203989971U (en) | Preliminary sedimentation concentrates reclamation set | |
| CN206355722U (en) | A kind of integrative water purifying device of water-saving and emission-reducing | |
| CN104128020B (en) | Preliminary sedimentation concentrates reuse tank and treatment process thereof | |
| CN217265385U (en) | Comprehensive dehydration machine room system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |